CN204959018U - High alumina fly ash system graphite alkene alloy material's apparatus for producing - Google Patents
High alumina fly ash system graphite alkene alloy material's apparatus for producing Download PDFInfo
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- CN204959018U CN204959018U CN201520674875.XU CN201520674875U CN204959018U CN 204959018 U CN204959018 U CN 204959018U CN 201520674875 U CN201520674875 U CN 201520674875U CN 204959018 U CN204959018 U CN 204959018U
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Abstract
The utility model relates to a graphite alkene alloy field especially relates to high alumina fly ash system graphite alkene alloy material's apparatus for producing, and the device includes: high temperature high alumina fly ash island, the washing island, the desiliconization island, the desulfurization island, the aluminum alloy island, the hydroxide island, the silica island, the iron oxide island, the titanium dioxide island, graphite alkene powder island, the auxiliary material island, the synthetic island of graphite alkene alloy, long -range explosion -proof surveillance center island, high temperature high alumina fly ash island, the washing island, the desiliconization island, the desulfurization island, the aluminum alloy island connects gradually, the washing island is connected with the hydroxide island, the desiliconization island is connected with the silica island, desulfurization island and iron oxide island, the titanium dioxide island is connected, the silica island, the iron oxide island, the titanium dioxide island, the aluminum alloy island, graphite alkene powder island, the auxiliary material island is synthesized the island with graphite alkene alloy and is connected, online explosion -proof control is carried out on long -range explosion -proof surveillance center island, the utility model discloses beneficial effect lies in: utilize high alumina fly ash resource, concentrated sulfuric acid cyclic utilization, it is with low costs to prepare graphite alkene alloy material.
Description
Technical field
The utility model relates to Graphene alloy field, particularly relates to the production equipment of aluminous fly-ash Graphene alloy material.
Background technology
As the type material that intensity is maximum up to now, conductivity is best, Graphene is the problem that the multinational scientists such as China, USA and Europe competitively study always.Graphene belongs to nanometer materials, and therefore itself just has the due surfactivity state of nanoparticle, is easily combined with other materials particle.The topmost application of current nanoparticle is that while remaining Graphene superperformance, its intensity significantly improves as packing material during other non-nano material modifications.
Graphene production cost is expensive, and cost ratio gold is high doubly a lot, has a strong impact on Graphene Industry Promotion application.
China is annual produces several ten million tons of aluminous fly-ashs, the current overwhelming majority is stacked without any process is discarded, while taking a large amount of soil, also form second time pollute, especially contaminate environment (as underground water, airborne dust), and the oxide compounds such as the aluminium be rich in aluminous fly-ash, silicon, iron, titanium, lithium are not utilized effectively, form the wasting of resources.
Utility model content
The utility model is overcome above-mentioned weak point, and object is to utilize aluminous fly-ash to produce Graphene alloy material, reduces environmental pollution, reduces Graphene alloy production cost.
The utility model achieves the above object by the following technical programs: the production equipment of aluminous fly-ash Graphene alloy material, comprise: high temperature aluminous fly-ash island, washing island, desiliconization island, desulfurization island, aluminium alloy island, oxyhydroxide island, titanium dioxide silicon island, ferric oxide island, titanium dioxide island, Graphene powder island, auxiliary material island, Graphene alloy synthesis island, long-distance anti-explosion Surveillance center island, high temperature aluminous fly-ash island, washing island, desiliconization island, desulfurization island, aluminium alloy island connects successively, washing island is connected with oxyhydroxide island, desiliconization island is connected with titanium dioxide silicon island, desulfurization island and ferric oxide island, titanium dioxide island connects, titanium dioxide silicon island, ferric oxide island, titanium dioxide island, aluminium alloy island, Graphene powder island, auxiliary material island and Graphene alloy synthesize island and are connected, long-distance anti-explosion Surveillance center carries out online anti-explosion surveillance in island.
As preferably, wash island and comprise high temperature aluminous fly-ash intelligence handling machinery, electric mixer I, pure clean water basin, hypergravity washing pool, electric motor I, solid-liquid separator I; High temperature aluminous fly-ash intelligence handling machinery, pure clean water basin are connected with washing pool, electric mixer I is provided with in washing pool, electric mixer I is connected with electric motor I, is connected bottom washing pool with solid-liquid separator I, and solid-liquid separator I is connected with desiliconization island, oxyhydroxide island; Clear water is sent in washing pool by high temperature aluminous fly-ash intelligence handling machinery by high temperature aluminous fly-ash, pure clean water basin, electric motor I is sent in solid-liquid separator I after driving electric mixer I pair of high temperature aluminous fly-ash and clear water to carry out fully stirring and is carried out solid-liquid separation, water-soluble hydroxide solution send oxyhydroxide island, and water-fast solid matter send the desiliconization of desiliconization island.
As preferably, desiliconization island comprises vitriol oil tank, electric mixer II, electric motor II, desiliconization pond, electric heater, solid-liquid separator II; Described desiliconization pond is connected with solid-liquid separator I, vitriol oil tank, electric mixer II is provided with in desiliconization pond, electric mixer II is connected with electric motor II, desiliconization is provided with electric heater bottom pond, bottom, desiliconization pond is connected with solid-liquid separator II, and solid-liquid separator II is connected with desulfurization island, titanium dioxide silicon island; The water-fast solid matter that solid-liquid separator I is separated is sent in desiliconization pond together with the vitriol oil in vitriol oil tank, electric motor II is sent in solid-liquid separator II after driving electric mixer II pair of solid matter and the vitriol oil to carry out fully stirring and is carried out solid-liquid separation, the solution being dissolved in the vitriol oil sends into desulfurization island, and the solid matter being insoluble to the vitriol oil send titanium dioxide silicon island.
As preferably, aluminium alloy island comprises alchlor intelligence handling machinery, carbon black intelligence handling machinery, CO tank, plasma-catalytic device, catalysis core reaction chamber, long-distance anti-explosion monitor, filtering net, CO
2trapping system, CO
2separator; Described alchlor intelligence handling machinery, carbon black intelligence handling machinery, CO tank are connected with plasma-catalytic device, and plasma-catalytic device is connected with catalysis core reaction chamber, is provided with filtering net, catalysis core reaction chamber and CO in catalysis core reaction chamber
2trapping system, aluminium alloy island connect, CO
2trapping system and CO
2separator connects, CO
2separator is connected with carbon black intelligence handling machinery, long-distance anti-explosion monitor on-line monitoring catalysis core reaction chamber.
The beneficial effects of the utility model are: one is effectively utilize aluminous fly-ash resource, reduce aluminous fly-ash pile up cause water pollutions, Land pollution, effectively utilize the oxide compound such as aluminium, silicon, iron, titanium, lithium be rich in aluminous fly-ash, avoid the wasting of resources; Two is vitriol oil recycles, reduces production cost; Three is produce comparatively current other technology both at home and abroad of Graphene alloy material to reduce costs more than 60%, enables Graphene alloy material realize applying.
Accompanying drawing explanation
Fig. 1 is the structural representation of the utility model device;
Fig. 2 is the structural representation on washing island of the present utility model;
Fig. 3 is the structural representation on desiliconization island of the present utility model;
Fig. 4 is the structural representation on aluminium alloy island of the present utility model;
Fig. 5 is the process flow sheet of the utility model embodiment 2.
Embodiment
Below in conjunction with specific embodiment, the utility model is described further, but protection domain of the present utility model is not limited in this:
Embodiment 1: as shown in Figure 1, the production equipment of aluminous fly-ash Graphene alloy material, comprise: high temperature aluminous fly-ash island, washing island, desiliconization island, desulfurization island, aluminium alloy island, oxyhydroxide island, titanium dioxide silicon island, ferric oxide island, titanium dioxide island, Graphene powder island, auxiliary material island, Graphene alloy synthesis island, long-distance anti-explosion Surveillance center island, high temperature aluminous fly-ash island, washing island, desiliconization island, desulfurization island, aluminium alloy island connects successively, washing island is connected with oxyhydroxide island, desiliconization island is connected with titanium dioxide silicon island, desulfurization island and ferric oxide island, titanium dioxide island connects, titanium dioxide silicon island, ferric oxide island, titanium dioxide island, aluminium alloy island, Graphene powder island, auxiliary material island and Graphene alloy synthesize island and are connected, long-distance anti-explosion Surveillance center carries out online anti-explosion surveillance in island.
High temperature aluminous fly-ash island, comprises the combustion high alumina coal burning boiler of thermoelectricity, and the temperature of combustion of combustion high alumina coal burning boiler is 900-1600 DEG C.
As shown in Figure 2, wash island and comprise high temperature aluminous fly-ash intelligence handling machinery, electric mixer I, pure clean water basin, hypergravity washing pool, electric motor I, solid-liquid separator I; High temperature aluminous fly-ash intelligence handling machinery, pure clean water basin are connected with washing pool, electric mixer I is provided with in washing pool, electric mixer I is connected with electric motor I, is connected bottom washing pool with solid-liquid separator I, and solid-liquid separator I is connected with desiliconization island, oxyhydroxide island; Clear water is sent in washing pool by high temperature aluminous fly-ash intelligence handling machinery by high temperature aluminous fly-ash, pure clean water basin, electric motor I is sent in solid-liquid separator I after driving electric mixer I pair of high temperature aluminous fly-ash and clear water to carry out fully stirring and is carried out solid-liquid separation, water-soluble hydroxide solution send oxyhydroxide island, and water-fast solid matter send the desiliconization of desiliconization island.This device by the high temperature aluminous fly-ash of 900-1600 DEG C send into washing pool, slough the oxide compound that aluminous fly-ash is water-soluble, as oxidation receive, potassium oxide, magnesium oxide, calcium oxide, Lithium Oxide 98min.Water-soluble oxide compound is sent into oxyhydroxide island and extracts oxyhydroxide, as sodium hydroxid, potassium hydroxide, magnesium hydroxide, calcium hydroxide, lithium hydroxide.Water-fast aluminous fly-ash sends into the desiliconization of desiliconization island.
As shown in Figure 3, desiliconization island comprises vitriol oil tank, electric mixer II, electric motor II, desiliconization pond, electric heater, solid-liquid separator II; Described desiliconization pond is connected with solid-liquid separator I, vitriol oil tank, electric mixer II is provided with in desiliconization pond, electric mixer II is connected with electric motor II, desiliconization is provided with electric heater bottom pond, bottom, desiliconization pond is connected with solid-liquid separator II, and solid-liquid separator II is connected with desulfurization island, titanium dioxide silicon island; The water-fast solid matter that solid-liquid separator I is separated is sent in desiliconization pond together with the vitriol oil in vitriol oil tank, electric motor II is sent in solid-liquid separator II after driving electric mixer II pair of solid matter and the vitriol oil to carry out fully stirring and is carried out solid-liquid separation, the solution being dissolved in the vitriol oil sends into desulfurization island, and the solid matter being insoluble to the vitriol oil send titanium dioxide silicon island.This device adopts silicon oxide to be insoluble to the vitriol oil, and the principle that aluminum oxide, ferric oxide, titanium oxide are dissolved in the vitriol oil carries out separation desiliconization.The hydrosulfate that the aluminous fly-ash being dissolved in the vitriol oil after desiliconization produces is sent into desulfurization island.
Table 1 is the dissolving information slip of oxide compound and the vitriol oil:
Table 1
Desulfurization island, comprises electric smelting furnace.The temperature of desulfurization island electric smelting furnace is 650-2300 DEG C of desulfurization, produces ferric oxide, titanium dioxide, aluminium sesquioxide; Ferric oxide send ferric oxide island, titanium dioxide send titanium dioxide island, and aluminium sesquioxide send aluminium alloy island, and the oxysulfide pinching vitriol oil that desulfurization island produces recycles.Wherein, the separation temperature of ferric oxide is 650-900 DEG C, and the separation temperature of titanium oxide is 1550-1600 DEG C, and the separation temperature of aluminium sesquioxide is 2000-2400 DEG C.
As shown in Figure 4, aluminium alloy island comprises alchlor intelligence handling machinery, carbon black intelligence handling machinery, CO tank, plasma-catalytic device, catalysis core reaction chamber, long-distance anti-explosion monitor, filtering net, CO
2trapping system, CO
2separator; Described alchlor intelligence handling machinery, carbon black intelligence handling machinery, CO tank are connected with plasma-catalytic device, and plasma-catalytic device is connected with catalysis core reaction chamber, is provided with filtering net, catalysis core reaction chamber and CO in catalysis core reaction chamber
2trapping system, aluminium alloy island connect, CO
2trapping system and CO
2separator connects, CO
2separator is connected with carbon black intelligence handling machinery, long-distance anti-explosion monitor on-line monitoring catalysis core reaction chamber.
Graphene powder island, comprises Graphene powder intelligence delivery system.
Auxiliary material island, comprises auxiliary material intelligence delivery system, will as silver, tin, copper, zinc, carbon black or gac, and plastics organic substance, sends into Graphene alloys synthesize islands as one or more in alkene, polyimide.
Graphene alloy synthesis island, Graphene alloy product is produced according to different material formula, as: Graphene aluminium alloy, Graphene titanium alloy, Graphene lithium alloy, Graphene titanium silicon, Graphene silver carbon alloy, Graphene aluminium copper iron, Graphene plastic-aluminum alloy.
Long-distance anti-explosion Surveillance center island, comprises and carries out online anti-explosion surveillance to each link of total system, and real-time monitoring temperature, pressure, and monitors surrounding enviroment.
Based on the production technique of the aluminous fly-ash Graphene alloy material of said apparatus, comprise the following steps:
1) open each system power switch, online anti-explosion surveillance is carried out to each link of total system in long-distance anti-explosion Surveillance center island, and real-time monitoring temperature, pressure, and monitors surrounding enviroment;
2) aluminous fly-ash of 900-1600 DEG C of high temperature in high temperature aluminous fly-ash island is sent into washing pool, slough the oxide compound that aluminous fly-ash is water-soluble, water-soluble hydroxide solution send oxyhydroxide island, and water-fast solid matter send the desiliconization of desiliconization island;
3) desiliconization island is by the water-fast solid matter of previous step and strong sulfuric acid response, and the solution being dissolved in the vitriol oil sends into desulfurization island, and the solid matter being insoluble to the vitriol oil send titanium dioxide silicon island;
Desiliconization island completes main reaction:
Al
2O
3+3H
2SO
4——Al
2(SO
4)
3+3H
2O(1)
Fe
2O
3+3H
2SO
4——Fe
2(SO
4)
3+3H
2O(2)
TiO
2+H
2SO
4——TiOSO
4+H
2O(3)
4) electric smelting furnace desulfurization under the environment of 650-2300 DEG C of desulfurization island, produces ferric oxide, titanium dioxide, aluminium sesquioxide; Ferric oxide send ferric oxide island, titanium dioxide send titanium dioxide island, and aluminium sesquioxide send aluminium alloy island, and the oxysulfide pinching vitriol oil that desulfurization island produces recycles; The ferric oxide that desulfurization island produces, titanium dioxide, aluminium sesquioxide adopt different separation temperatures to be separated, the separation temperature of ferric oxide is 650-900 DEG C, the separation temperature of titanium oxide is 1550-1600 DEG C, and the separation temperature of aluminium sesquioxide is 2000-2400 DEG C;
Desulfurization island completes main reaction:
Fe
2(SO
4)
3——Fe
2O
3+2SO
2+SO
3+O
2(4)
2TiOSO
4——Ti
2O+SO
3(5)
Al
2(SO
4)
3——Al
2O
3+3SO
3(6)
5) aluminium sesquioxide previous step carried of aluminium alloy island is under plasma environment, react with carbon, Carbon monoxide reduction, produce high purity aluminum alloy: open CO tank valve, CO and aluminium sesquioxide and carbon black to be sent in plasma-catalytic device after catalysis, send catalysis further in catalysis core reaction chamber, temperature of reaction is 2000-2300 DEG C, and pure aluminum send Graphene alloy to synthesize island, and gas send CO after net filtration after filtration
2trapping system trapping CO
2, the CO be captured
2send CO
2separator is separated and obtains carbon black, and carbon black send carbon black intelligence handling machinery, reaches CO
2recycle; Temperature, pressure, gaseous constituent in long-distance anti-explosion monitor on-line monitoring catalysis core reaction chamber 9;
Aluminium alloy island completes main reaction:
2Al
2O
3+3C——4Al+3CO
2(7)
Al
2O
3+3CO——2Al+3CO
2(8)
6) by the aluminium alloy on the titanium dioxide on the ferric oxide on the silicon-dioxide of titanium dioxide silicon island, ferric oxide island, titanium dioxide island, aluminium alloy island, the Graphene powder on Graphene powder island, the auxiliary material on auxiliary material island, intelligence is transported to Graphene alloy synthesis island and produces Graphene alloy material product in proportion.
Embodiment 2: the utility model also can adopt aluminous fly-ash and carbon, carbon monoxide directly to carry out reduction reaction under plasma environment, metal oxide in aluminous fly-ash is become elemental metals atom fast, as pure aluminum, elemental silicon, fe, simple substance titanium, simple substance lithium, simple substance calcium etc., produce Graphene alloy material product.
The production equipment of aluminous fly-ash Graphene alloy material, comprising: aluminous fly-ash handling machinery, carbon source handling machinery, CO tank, plasma-catalytic device, catalysis core reactor, filtering net, long-distance anti-explosion monitor, residual-heat exchanger power generation system, CO
2trapping system, CO
2separator, melting separator, Graphene powder island, Graphene alloy synthesis island, auxiliary material island; Described aluminous fly-ash handling machinery, carbon source handling machinery, CO tank are connected with plasma-catalytic device, plasma-catalytic device is connected with catalysis core reactor, be provided with filtering net in catalysis core reactor, catalysis core is connected with residual-heat exchanger power generation system, residual-heat exchanger power generation system and CO
2trapping system connects, CO
2trapping system and CO
2separator connects, CO
2separator is connected with carbon black intelligence handling machinery, and long-distance anti-explosion monitor on-line monitoring catalysis core reaction chamber, catalysis core reactor is also connected with melting separator, and melting separator, Graphene powder island, auxiliary material island are synthesized island with Graphene alloy and be connected.
The production technique of aluminous fly-ash Graphene alloy material comprises the following steps:
The first step, open CO tank valve, aluminous fly-ash handling machinery, carbon source handling machinery, CO and aluminous fly-ash, carbon source to be sent in plasma-catalytic device after catalysis, send catalysis further in catalysis core reaction chamber, the elemental metals material produced send melting separator, be separated according to elemental metals material different melting points, obtain as pure aluminum, elemental silicon, fe, simple substance titanium, simple substance lithium, simple substance calcium etc.
Produce the main reaction that pure aluminum completes:
2Al
2O
3+3C——4Al+3CO
2(9)
Al
2O
3+3CO——2Al+3CO
2(10)
Produce the main reaction that elemental silicon (silicon single crystal, polysilicon) completes:
SiO
2+C——Si+CO
2(11)
SiO
2+2CO——Si+2CO
2(12)
Produce the main reaction that fe completes:
2Fe
2O3+3C——4Fe+3CO
2(13)
Fe
2O3+3CO——2Fe+3CO
2(14)
Produce the main reaction that simple substance titanium completes:
TiO
2+C——Ti+CO
2(15)
TiO
2+2CO——Ti+2CO
2(16)
Produce the main reaction that simple substance lithium completes:
2Li
2O+C——4Li+CO
2(17)
Li
2O+CO——2Li+CO
2(18)
Produce the main reaction that simple substance calcium completes:
2CaO+C——2Ca+CO
2(19)
CaO+CO——Ca+CO
2(20)
The temperature of the catalytic reduction reaction of preferred plasma-catalytic device, catalysis core reaction chamber is 2000-2300 DEG C.
Second step, send residual-heat exchanger power generation system to generate electricity by after the high-temperature gas of the catalytic reduction reaction of catalysis core reaction chamber after filtration net filtration, the gas through the cooling of residual-heat exchanger power generation system send CO
2trapping system trapping CO
2, send CO
2separator is separated, and produces carbon black and send carbon black intelligence handling machinery, reach CO
2recycle.
The carbon source of carbon source handling machinery conveying also can be gac, high alumina coke, high alumina coking coal.
3rd step, open long-distance anti-explosion monitor power switch, temperature, pressure, gaseous constituent in on-line monitoring catalysis core reaction chamber.
4th step, by elemental metals atom, as pure aluminum, elemental silicon, fe, simple substance titanium, simple substance lithium, simple substance calcium and Graphene powder, auxiliary material are sent into Graphene alloy by required formula rate and synthesized island, produce Graphene alloy product, as Graphene lithium alloy, Graphene aluminium alloy, Graphene titanium alloy, Graphene silver carbon alloy, Graphene aluminum silicon alloy, Graphene ferroaluminium, Graphene aluminum-copper alloy, Graphene titanium zinc alloy, Graphene plastic-aluminum alloy etc.
The know-why being specific embodiment of the utility model and using described in above; if according to the change that conception of the present utility model is done; its function produced do not exceed that specification sheets and accompanying drawing contain yet spiritual time, protection domain of the present utility model must be belonged to.
Claims (4)
1. the production equipment of aluminous fly-ash Graphene alloy material, it is characterized in that comprising: high temperature aluminous fly-ash island, washing island, desiliconization island, desulfurization island, aluminium alloy island, oxyhydroxide island, titanium dioxide silicon island, ferric oxide island, titanium dioxide island, Graphene powder island, auxiliary material island, Graphene alloy synthesis island, long-distance anti-explosion Surveillance center island, high temperature aluminous fly-ash island, washing island, desiliconization island, desulfurization island, aluminium alloy island connects successively, washing island is connected with oxyhydroxide island, desiliconization island is connected with titanium dioxide silicon island, desulfurization island and ferric oxide island, titanium dioxide island connects, titanium dioxide silicon island, ferric oxide island, titanium dioxide island, aluminium alloy island, Graphene powder island, auxiliary material island and Graphene alloy synthesize island and are connected, long-distance anti-explosion Surveillance center carries out online anti-explosion surveillance in island.
2. the production equipment of aluminous fly-ash Graphene alloy material according to claim 1, it is characterized in that, washing island comprises high temperature aluminous fly-ash intelligence handling machinery, electric mixer I, pure clean water basin, hypergravity washing pool, electric motor I, solid-liquid separator I; High temperature aluminous fly-ash intelligence handling machinery, pure clean water basin are connected with washing pool, electric mixer I is provided with in washing pool, electric mixer I is connected with electric motor I, is connected bottom washing pool with solid-liquid separator I, and solid-liquid separator I is connected with desiliconization island, oxyhydroxide island; Clear water is sent in washing pool by high temperature aluminous fly-ash intelligence handling machinery by high temperature aluminous fly-ash, pure clean water basin, electric motor I is sent in solid-liquid separator I after driving electric mixer I pair of high temperature aluminous fly-ash and clear water to carry out fully stirring and is carried out solid-liquid separation, water-soluble hydroxide solution send oxyhydroxide island, and water-fast solid matter send the desiliconization of desiliconization island.
3. the production equipment of aluminous fly-ash Graphene alloy material according to claim 1, is characterized in that, desiliconization island comprises vitriol oil tank, electric mixer II, electric motor II, desiliconization pond, electric heater, solid-liquid separator II; Described desiliconization pond is connected with solid-liquid separator I, vitriol oil tank, electric mixer II is provided with in desiliconization pond, electric mixer II is connected with electric motor II, desiliconization is provided with electric heater bottom pond, bottom, desiliconization pond is connected with solid-liquid separator II, and solid-liquid separator II is connected with desulfurization island, titanium dioxide silicon island; The water-fast solid matter that solid-liquid separator I is separated is sent in desiliconization pond together with the vitriol oil in vitriol oil tank, electric motor II is sent in solid-liquid separator II after driving electric mixer II pair of solid matter and the vitriol oil to carry out fully stirring and is carried out solid-liquid separation, the solution being dissolved in the vitriol oil sends into desulfurization island, and the solid matter being insoluble to the vitriol oil send titanium dioxide silicon island.
4. the production equipment of aluminous fly-ash Graphene alloy material according to claim 1, it is characterized in that, aluminium alloy island comprises aluminium sesquioxide intelligence handling machinery, carbon black intelligence handling machinery, CO tank, plasma-catalytic device, catalysis core reaction chamber, long-distance anti-explosion monitor, filtering net, CO
2trapping system, CO
2separator; Described aluminium sesquioxide intelligence handling machinery, carbon black intelligence handling machinery, CO tank are connected with plasma-catalytic device, and plasma-catalytic device is connected with catalysis core reaction chamber, is provided with filtering net, catalysis core reaction chamber and CO in catalysis core reaction chamber
2trapping system, aluminium alloy island connect, CO
2trapping system and CO
2separator connects, CO
2separator is connected with carbon black intelligence handling machinery, long-distance anti-explosion monitor on-line monitoring catalysis core reaction chamber.
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|---|---|---|---|
| CN201520674875.XU CN204959018U (en) | 2015-09-02 | 2015-09-02 | High alumina fly ash system graphite alkene alloy material's apparatus for producing |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105039773A (en) * | 2015-09-02 | 2015-11-11 | 程礼华 | Production device and process of graphene alloy materials prepared from high-alumina fly ash |
| CN105624539A (en) * | 2016-03-03 | 2016-06-01 | 程礼华 | Carbon and oxygen circulation device for graphene steel alloy and technology thereof |
-
2015
- 2015-09-02 CN CN201520674875.XU patent/CN204959018U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105039773A (en) * | 2015-09-02 | 2015-11-11 | 程礼华 | Production device and process of graphene alloy materials prepared from high-alumina fly ash |
| CN105039773B (en) * | 2015-09-02 | 2017-01-11 | 程礼华 | Production device and process of graphene alloy materials prepared from high-alumina fly ash |
| CN105624539A (en) * | 2016-03-03 | 2016-06-01 | 程礼华 | Carbon and oxygen circulation device for graphene steel alloy and technology thereof |
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